CA2395893A1 - Fibrous sheet binders - Google Patents
Fibrous sheet binders Download PDFInfo
- Publication number
- CA2395893A1 CA2395893A1 CA002395893A CA2395893A CA2395893A1 CA 2395893 A1 CA2395893 A1 CA 2395893A1 CA 002395893 A CA002395893 A CA 002395893A CA 2395893 A CA2395893 A CA 2395893A CA 2395893 A1 CA2395893 A1 CA 2395893A1
- Authority
- CA
- Canada
- Prior art keywords
- binder
- fibrous sheet
- anionic polymer
- polymer
- group
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Abandoned
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
- C09J179/00—Adhesives based on macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing nitrogen, with or without oxygen, or carbon only, not provided for in groups C09J161/00 - C09J177/00
- C09J179/02—Polyamines
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/71—Mixtures of material ; Pulp or paper comprising several different materials not incorporated by special processes
- D21H17/72—Mixtures of material ; Pulp or paper comprising several different materials not incorporated by special processes of organic material
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H13/00—Pulp or paper, comprising synthetic cellulose or non-cellulose fibres or web-forming material
- D21H13/36—Inorganic fibres or flakes
- D21H13/38—Inorganic fibres or flakes siliceous
- D21H13/40—Inorganic fibres or flakes siliceous vitreous, e.g. mineral wool, glass fibres
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/20—Macromolecular organic compounds
- D21H17/21—Macromolecular organic compounds of natural origin; Derivatives thereof
- D21H17/24—Polysaccharides
- D21H17/28—Starch
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/20—Macromolecular organic compounds
- D21H17/33—Synthetic macromolecular compounds
- D21H17/34—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
- D21H17/41—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing ionic groups
- D21H17/42—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing ionic groups anionic
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/20—Macromolecular organic compounds
- D21H17/33—Synthetic macromolecular compounds
- D21H17/34—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
- D21H17/41—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing ionic groups
- D21H17/44—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing ionic groups cationic
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/20—Macromolecular organic compounds
- D21H17/33—Synthetic macromolecular compounds
- D21H17/46—Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
- D21H17/54—Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds obtained by reactions forming in the main chain of the macromolecule a linkage containing nitrogen
- D21H17/56—Polyamines; Polyimines; Polyester-imides
Abstract
A method and composition are disclosed for providing a two-part polymer binder additive for a fibrous sheet for improving both its strength and durability. The two-part polymer binder may be added to augment organic binders to increase board strength and durability or to reduce the amount of organic binder required.
The polymers may also be added in place of conventional organic binders or added in addition to organic binders to improve sag resistance and fibrous sheet performance.
The polymers may also be added in place of conventional organic binders or added in addition to organic binders to improve sag resistance and fibrous sheet performance.
Description
The results of mechanical testing:
a*=O.SOMPa, dry state a*=0..20MPa, wet state.
Example 3 The IPEC modified composition was prepared as for Example 1, except that the 0.9g of starch was added instead of 1.8g.
The results of mechanical testing:
a*=0.38MPa, dry state 6*=0.1 OMPa, wet state (a*-value for composition including 0.9g of starch and not containing IPEC
6*=0.20MPa, dry state a*=O.OSMPa, wet state).
Example 4 The IPEC modified composition was prepared as for Example 2, except that the composition included 0.9g of starch instead of 1.8g.
The results of mechanical testing:
a*=O.SOMPa, dry state 6*=0.25MPa, wet state.
Example 5 The IPEC modified composition was prepared as for Example l, except that the composition included 0.9g of starch and 0.48g IPEC(PAA-PDADMAC), ~ as a modifier. l2ml O.1N aqueous solution of sodium poly(acrylate) (NaPA) (O.llg of S NaPA), 24m1 O.1N aqueous solution of PAA (0.173g of PAA) and 12m1 O.1N
aqueous solution of poly(N,N-dimethyl-N,N-diallylammonium chloride) (PDADMAC) (0.194g of PDADMAC) were added under stirring. 0.018g of flocculant in the form of 0.2wt.% aqueous dispersion was added last.
The results of mechanical testing:
a*=0.60MPa, dry state a*=0.30MPa, wet state.
Example 6 The IPEC modified composition was prepared as for Example l, except that 1 S the composition did not contain starch and 1.8g IPEC(PAA-PDADMAC), ~ was added as a modifier. 44.0 ml. 0.1N aqueous solution of sodium poly(acrylate) (NaPA) (0.42g of NaPA), 88.0 ml O.1N aqueous solution of PAA (0.63g of PAA) and 44.0 ml O.1N aqueous solution of poly(N,N-dimethyl-N,N-diallylammonium chloride) (PDADMAC) (0.71 g of PDADMAC) were added to the composition under stirring.
0.018g of flocculant in the form of 0.2wt.% aqueous dispersion was added last.
The results of mechanical testing:
a*=0.70MPa, dry state 6*=0.40MPa, wet state.
IS
The results of mechanical testing of the compositions in terms of the values of stress at break (MPa) are listed in Table 3 and Figure 4. Figure 4 and Table 3 illustrate the effects of starch and IPEC modifier compared to starch alone and IPEC alone, on the mechanical characteristics of the composition prepared in the "brewing regime."
Table 3 IPEC Data Starch IPEC Total binderStress at Stress (g) (g) (g) break at break a* dry (Mpa)6* wet (Mpa) Control 0 0.5 0.5 0.4 0.3 IPEC alone0 0.9 0.9 0.5 0.35 0 1.2 1.2 0.6 0.4 0 1.8 1.8 0.7 0.4 0 2.7 2.7 0.85 0.45 Control2 0.5 0 0.5 0.15 0.1 Starch 0.9 0 0.9 _ _0.2 0.05 alone 1.2 0 1.2 0.25 0.0?
1.8 0 1.8 0.35 0.1 2.7 0 2.7 0.55 0.25 Combination0.5 _ 0.3 0.8 0.5 3 ~
0.5 g 0.5 0.5 I 0.65 0.4 Starch plus varied0.5 0.9 1.4 0.7 0.4 IPEC
Combination0.9 0.15 1.05 0.38 0.1 0.9 g 0.9 0.3 1.2 0.5 0.25 Starch 0.9 0.5 1.4 0.6 0.3 plus varied IPEC
Combination1.2 0.3 1.5 0.5 0.25 1.2 g 1.2 0.5 1.7 _0.6 0.3 Starch plus varied1.2 0.9 2.1 0.7 0.35 IPEC
Combination1.8 0.15 1.95 0.45 0.15 I
1.8 g 1.8 0.3 2.1 0.5 0.2 Starch 1.8 0.5 2.3 0.6 0.25 plus varied I PEC
PESC (Surfactant) Examples In the following examples, polyelectrolyte-surfactant complexes (PESC) additives where added to a basic mix of fiberboard components. The mechanical characteristics of the compositions containing different amounts of starch and PESC
S additives are illustrated in the examples. The basic components for the fiberboard were prepared in the brewing regime and were added in the following amounts:
Newsprint 6.6g Mineral Wool 4.5g Perlite 17.1 g Starch 0-2.7g Flocculant 0.018g 0.001 N KCl aqueous solution 1000g Example 7 Mineral wool, starch, perlite and newspaper were mixed as described in Example 1. Polyelectrolyte-surfactant complex (PESC) formed by partially neutralized poly(acrylic acid) (PAA) and dodecyltrimethylammonium bromide (DDTMAD) was used as a modifier. 3.6m1 0.1N aqueous solution of sodium poly(acrylate) (NaPA) (0.034g of NaPA) and 7.2m1 O.1N aqueous solution of PAA
(0.052g of PAA) were added under stirring. 9.0 ml 0.04N aqueous solution of DDTMAB (0.11g) was added and stirred for 2 minutes. Thus, 0.2g of PESC(PAA-DDTMAB), ~=[carboxylic groups]/[amine groups]=3.0 was added to the composition as a modifier. 0.018g of flocculant in the form of 0.2wt.% aqueous dispersion was added last by a plastic syringe.
The mixture was filtered with a Buchner funnel and dried in the "starch-brewing" regime as described in Example 1.
The results of mechanical testing:
a*=O.SOMPa, dry state a*=0.30MPa, wet state.
Example 8 The PESO modified composition was prepared as described in Example 7, except that DDTMAB was added first.
The results of mechanical testing:
a*=0.47MPa, dry state 6*=0.29MPa, wet state.
Example 9 The PESC modified composition was prepared as described in Example 7, except that 0.144g of PESC(PAA-DDTMAB), ~=[carboxylic groups]/[amine groups]=1.0, was added as a modifier. 3.6m1 O.1N aqueous solution of sodium poly(acrylate) (NaPA) (0.034g of NaPA) and after that, 9.0 ml 0.04N aqueous solution of DDTMAB (0.11 g) was added under stirnng.
The results of mechanical testing:
6*=O.SOMPa, dry state 6*=0.30MPa, wet state.
Example 10 In this example the PESC was added without the addition of starch. The stoichiometric complex formed by sodium polyacrylate (NaPA) and dodecyltrimethylammonium bromide (DDTMAB) named as PESC, cp=1, as well as the nonstoichiometric PESC, cp=3.0 containing a threefold excess of poly(acrylic acid), were used.
Newsprint, mineral wool and perlite were mixed in 1000 ml of warm (40° C) 0.001 N KCl aqueous solution under stirring. Then, 0.1 N NaPA aqueous solution and the corresponding amount of 0.04 N aqueous solution of DDTMAB were added under stirring for about 2-3 minutes. In the case of PESC, cp=1 the equimolar amounts of NaPA and DDTMAB were added. In the case of PESC, cp=3.0, the predetermined amount of 0.1 N aqueous solution of partially (one third) neutralized poly(acrylic acid), and corresponding amount of DDTMAB were consequently added under stirring for about 2-3 minutes. The flocculant in the form of 0.2 wt.% aqueous solution was added last by means of quick injecting it by plastic syringe.
The obtained mixtures were filtered with a Buchner funnel. The samples were enveloped in aluminum foil and kept at 177° C for 1 hour and unwrapped and dried at 177° C for 1 hour.
The wet compositions were prepared via equilibration with water vapor at 95% relative humidity (95 RH) saturated solution of KN03 in distilled water at 20° C) in the dessicator for 14 days. The samples were taken out the dessicator and were cut into 5-6 strips in the form of parallelepipeds with the length 100 mm, the width 10 mm and the thickness 8-10 mm. These strips were kept at 95 RH for 24 hours.
All the mechanical tests were carried out just after taking the strips out the dessicator using UTS-10 dynamometer (Germany) with the gauge length 70 mm.
The results of mechanical testing of the compositions in terms of the values of stress - at break, a* (MPa) are listed in the Table 4, control I and control 2 sections.
Table 4 illustrates the effects of PESC (PAA-DDTMAB) c~=1, cp=3.0 (cp=[PAA]/[DDTMAB]) as binders on the mechanical characteristics of the composition prepared in the "brewing regime." All samples contain 6.6 g of newsprint, 4.5 g of mineral wool, 17.1 g of perlite and 0.018 g of flocculant.
The samples did not contain starch. The samples were teste3 in dry and wet state.
The strengthening effect of PESC, cp=1 and PESC, c~3.0 used as co-binders together with the starch was also tested. The procedure of the preparation of the composition was the same as described above; however, the only difference is the variable amount of the starch. The samples for mechanical testing were prepared in the "starch brewing" regimes and were tested in the dry as well as in the wet state.
The results of mechanical testing of compositions containing the starch binder and PESC, cp=I or PESC, cp=3.0 co-binders are listed in Table 4 under combinations.
Table 4 and Figures 5 and 6 illustrate the joint action of starch binder and PESC
(PAA-DDTMAB) cp=1, cp=3.0 co-binder on the mechanical chaxacteristics of the compositions prepared in the brewing regime. All samples contained 6.6 g of newsprint, 4.5 g of mineral wool, 17.1 g of perlite and 0.018 g of flocculant.
The samples were tested in dry and wet state.
Table 4 Polyelectrolyte-Surfactant Complexes (PESC) Data Starch PESC Total binderStress at Stress (g) (g) (g) break at break 6* dry (Mpa)a* wet (Mpa) Controll 0 0.9 0.9 0.25 _0.1 PESC (1:l)0 1.2 _1.2 0.1 0.1 alone 0 1.8 1.8 0.15 0.1 0 2.7 2.7 0.3 0.3 Control2 0 0.9 0.9 0.2 0.1 ~
PESC (3:1)0 1.2 _ 1.2 0.25 0.1 alone 0 1.8 1.8 0.5 0.35 0 2.7 2.7 0.55 0.5 Control3 0.5 0 0.5 0.15 0.1 Starch 0.9 0 0.9 0.2 __ alone 0.05 (same 1.2 0 1.2 0.25 0.07 data as in Table 1.8 0 I_.8 0.35 O.I
a*=O.SOMPa, dry state a*=0..20MPa, wet state.
Example 3 The IPEC modified composition was prepared as for Example 1, except that the 0.9g of starch was added instead of 1.8g.
The results of mechanical testing:
a*=0.38MPa, dry state 6*=0.1 OMPa, wet state (a*-value for composition including 0.9g of starch and not containing IPEC
6*=0.20MPa, dry state a*=O.OSMPa, wet state).
Example 4 The IPEC modified composition was prepared as for Example 2, except that the composition included 0.9g of starch instead of 1.8g.
The results of mechanical testing:
a*=O.SOMPa, dry state 6*=0.25MPa, wet state.
Example 5 The IPEC modified composition was prepared as for Example l, except that the composition included 0.9g of starch and 0.48g IPEC(PAA-PDADMAC), ~ as a modifier. l2ml O.1N aqueous solution of sodium poly(acrylate) (NaPA) (O.llg of S NaPA), 24m1 O.1N aqueous solution of PAA (0.173g of PAA) and 12m1 O.1N
aqueous solution of poly(N,N-dimethyl-N,N-diallylammonium chloride) (PDADMAC) (0.194g of PDADMAC) were added under stirring. 0.018g of flocculant in the form of 0.2wt.% aqueous dispersion was added last.
The results of mechanical testing:
a*=0.60MPa, dry state a*=0.30MPa, wet state.
Example 6 The IPEC modified composition was prepared as for Example l, except that 1 S the composition did not contain starch and 1.8g IPEC(PAA-PDADMAC), ~ was added as a modifier. 44.0 ml. 0.1N aqueous solution of sodium poly(acrylate) (NaPA) (0.42g of NaPA), 88.0 ml O.1N aqueous solution of PAA (0.63g of PAA) and 44.0 ml O.1N aqueous solution of poly(N,N-dimethyl-N,N-diallylammonium chloride) (PDADMAC) (0.71 g of PDADMAC) were added to the composition under stirring.
0.018g of flocculant in the form of 0.2wt.% aqueous dispersion was added last.
The results of mechanical testing:
a*=0.70MPa, dry state 6*=0.40MPa, wet state.
IS
The results of mechanical testing of the compositions in terms of the values of stress at break (MPa) are listed in Table 3 and Figure 4. Figure 4 and Table 3 illustrate the effects of starch and IPEC modifier compared to starch alone and IPEC alone, on the mechanical characteristics of the composition prepared in the "brewing regime."
Table 3 IPEC Data Starch IPEC Total binderStress at Stress (g) (g) (g) break at break a* dry (Mpa)6* wet (Mpa) Control 0 0.5 0.5 0.4 0.3 IPEC alone0 0.9 0.9 0.5 0.35 0 1.2 1.2 0.6 0.4 0 1.8 1.8 0.7 0.4 0 2.7 2.7 0.85 0.45 Control2 0.5 0 0.5 0.15 0.1 Starch 0.9 0 0.9 _ _0.2 0.05 alone 1.2 0 1.2 0.25 0.0?
1.8 0 1.8 0.35 0.1 2.7 0 2.7 0.55 0.25 Combination0.5 _ 0.3 0.8 0.5 3 ~
0.5 g 0.5 0.5 I 0.65 0.4 Starch plus varied0.5 0.9 1.4 0.7 0.4 IPEC
Combination0.9 0.15 1.05 0.38 0.1 0.9 g 0.9 0.3 1.2 0.5 0.25 Starch 0.9 0.5 1.4 0.6 0.3 plus varied IPEC
Combination1.2 0.3 1.5 0.5 0.25 1.2 g 1.2 0.5 1.7 _0.6 0.3 Starch plus varied1.2 0.9 2.1 0.7 0.35 IPEC
Combination1.8 0.15 1.95 0.45 0.15 I
1.8 g 1.8 0.3 2.1 0.5 0.2 Starch 1.8 0.5 2.3 0.6 0.25 plus varied I PEC
PESC (Surfactant) Examples In the following examples, polyelectrolyte-surfactant complexes (PESC) additives where added to a basic mix of fiberboard components. The mechanical characteristics of the compositions containing different amounts of starch and PESC
S additives are illustrated in the examples. The basic components for the fiberboard were prepared in the brewing regime and were added in the following amounts:
Newsprint 6.6g Mineral Wool 4.5g Perlite 17.1 g Starch 0-2.7g Flocculant 0.018g 0.001 N KCl aqueous solution 1000g Example 7 Mineral wool, starch, perlite and newspaper were mixed as described in Example 1. Polyelectrolyte-surfactant complex (PESC) formed by partially neutralized poly(acrylic acid) (PAA) and dodecyltrimethylammonium bromide (DDTMAD) was used as a modifier. 3.6m1 0.1N aqueous solution of sodium poly(acrylate) (NaPA) (0.034g of NaPA) and 7.2m1 O.1N aqueous solution of PAA
(0.052g of PAA) were added under stirring. 9.0 ml 0.04N aqueous solution of DDTMAB (0.11g) was added and stirred for 2 minutes. Thus, 0.2g of PESC(PAA-DDTMAB), ~=[carboxylic groups]/[amine groups]=3.0 was added to the composition as a modifier. 0.018g of flocculant in the form of 0.2wt.% aqueous dispersion was added last by a plastic syringe.
The mixture was filtered with a Buchner funnel and dried in the "starch-brewing" regime as described in Example 1.
The results of mechanical testing:
a*=O.SOMPa, dry state a*=0.30MPa, wet state.
Example 8 The PESO modified composition was prepared as described in Example 7, except that DDTMAB was added first.
The results of mechanical testing:
a*=0.47MPa, dry state 6*=0.29MPa, wet state.
Example 9 The PESC modified composition was prepared as described in Example 7, except that 0.144g of PESC(PAA-DDTMAB), ~=[carboxylic groups]/[amine groups]=1.0, was added as a modifier. 3.6m1 O.1N aqueous solution of sodium poly(acrylate) (NaPA) (0.034g of NaPA) and after that, 9.0 ml 0.04N aqueous solution of DDTMAB (0.11 g) was added under stirnng.
The results of mechanical testing:
6*=O.SOMPa, dry state 6*=0.30MPa, wet state.
Example 10 In this example the PESC was added without the addition of starch. The stoichiometric complex formed by sodium polyacrylate (NaPA) and dodecyltrimethylammonium bromide (DDTMAB) named as PESC, cp=1, as well as the nonstoichiometric PESC, cp=3.0 containing a threefold excess of poly(acrylic acid), were used.
Newsprint, mineral wool and perlite were mixed in 1000 ml of warm (40° C) 0.001 N KCl aqueous solution under stirring. Then, 0.1 N NaPA aqueous solution and the corresponding amount of 0.04 N aqueous solution of DDTMAB were added under stirring for about 2-3 minutes. In the case of PESC, cp=1 the equimolar amounts of NaPA and DDTMAB were added. In the case of PESC, cp=3.0, the predetermined amount of 0.1 N aqueous solution of partially (one third) neutralized poly(acrylic acid), and corresponding amount of DDTMAB were consequently added under stirring for about 2-3 minutes. The flocculant in the form of 0.2 wt.% aqueous solution was added last by means of quick injecting it by plastic syringe.
The obtained mixtures were filtered with a Buchner funnel. The samples were enveloped in aluminum foil and kept at 177° C for 1 hour and unwrapped and dried at 177° C for 1 hour.
The wet compositions were prepared via equilibration with water vapor at 95% relative humidity (95 RH) saturated solution of KN03 in distilled water at 20° C) in the dessicator for 14 days. The samples were taken out the dessicator and were cut into 5-6 strips in the form of parallelepipeds with the length 100 mm, the width 10 mm and the thickness 8-10 mm. These strips were kept at 95 RH for 24 hours.
All the mechanical tests were carried out just after taking the strips out the dessicator using UTS-10 dynamometer (Germany) with the gauge length 70 mm.
The results of mechanical testing of the compositions in terms of the values of stress - at break, a* (MPa) are listed in the Table 4, control I and control 2 sections.
Table 4 illustrates the effects of PESC (PAA-DDTMAB) c~=1, cp=3.0 (cp=[PAA]/[DDTMAB]) as binders on the mechanical characteristics of the composition prepared in the "brewing regime." All samples contain 6.6 g of newsprint, 4.5 g of mineral wool, 17.1 g of perlite and 0.018 g of flocculant.
The samples did not contain starch. The samples were teste3 in dry and wet state.
The strengthening effect of PESC, cp=1 and PESC, c~3.0 used as co-binders together with the starch was also tested. The procedure of the preparation of the composition was the same as described above; however, the only difference is the variable amount of the starch. The samples for mechanical testing were prepared in the "starch brewing" regimes and were tested in the dry as well as in the wet state.
The results of mechanical testing of compositions containing the starch binder and PESC, cp=I or PESC, cp=3.0 co-binders are listed in Table 4 under combinations.
Table 4 and Figures 5 and 6 illustrate the joint action of starch binder and PESC
(PAA-DDTMAB) cp=1, cp=3.0 co-binder on the mechanical chaxacteristics of the compositions prepared in the brewing regime. All samples contained 6.6 g of newsprint, 4.5 g of mineral wool, 17.1 g of perlite and 0.018 g of flocculant.
The samples were tested in dry and wet state.
Table 4 Polyelectrolyte-Surfactant Complexes (PESC) Data Starch PESC Total binderStress at Stress (g) (g) (g) break at break 6* dry (Mpa)a* wet (Mpa) Controll 0 0.9 0.9 0.25 _0.1 PESC (1:l)0 1.2 _1.2 0.1 0.1 alone 0 1.8 1.8 0.15 0.1 0 2.7 2.7 0.3 0.3 Control2 0 0.9 0.9 0.2 0.1 ~
PESC (3:1)0 1.2 _ 1.2 0.25 0.1 alone 0 1.8 1.8 0.5 0.35 0 2.7 2.7 0.55 0.5 Control3 0.5 0 0.5 0.15 0.1 Starch 0.9 0 0.9 0.2 __ alone 0.05 (same 1.2 0 1.2 0.25 0.07 data as in Table 1.8 0 I_.8 0.35 O.I
3) 2.7 0 2.? 0.55 0.25 Combination0.9 0.15 1.05 0.2 0.15 0.9 g 0.9 0.3 1.2 0.3 0.15 Starch plus varied0.9 0.5 1.4 0.25 0.15 PESC (1:1)0.9 0.9 1.8 0.2 0.2 Combination0.9 0.1 S 1.05 0.2 0.2 0.9 g 0.9 0.3 1.2 0.4 0.2 Starch plus varied0.9 0.9 1.8 0.35 0.3 PESC (3:1)0.9 0.5 1.4 0.25 Combination1.8 0.1 S 1.95 0.4 0.2 1.8 g 1.8 0.3 2.1 0.5 0.25 Starch plus varied1.8 0.5 2.3 0.6 0.25 PESC (1:1) CombinationI.8 0.1 S 1.95 _0.5 0.3 1.8g Starch1.8 0.3 _ 2.1 0.6 0.25 plus varied1.8 0.5 2.3 0.8 0.3 -PESC (3:1)I.g ~ 0.9 ~ 2.7 0.6 0.3 ~
The strengthening effect of mixed IPEC+PESC co-binder in "starch brewing"
regime was also tested. Nonstoichiometric mixed IPEC (PAA-PDADMAC) + PESC
(PAA-DDTMAB), cp=3.0 was used. It was prepared as follows:
The predetermined amount of 0.1 N aqueous solution of partially neutralized (a+0,33) poly(acrylic acid) and then correspond-ing amount of 0.04 N aqueous solution of the equimolar mixture of PDADMAC and DDTMAB were added under stirring for about 2-3 minutes.
The compositions containing 0.9 g of the starch binder and different additives of mixed (IPEC+PESC), c~=3.0 co-binder were tested mechanically in the dry and wet S state. The results of the latest measurements are listed in Table 3. Table 3 illustrates the joint action of starch binder and mixed IPEC (PAA-PDADMAC) + PESC (PAA-DDTMAB), cp=3.0 (cp=[PAA]/[DDTMAB+PDADMAC] at [DDTMAB]=[PDADMAC]) co-binder on the mechanical characteristics of the compositions prepared in the "brewing" regime. All samples contained 6.6 g of newsprint, 4.5 g of mineral wool. 17.1 g of perlite and 0.018 g of flocculant.
The samples were tested in dry and wet state.
Table 5 IPEC and PESC Combinations as Starch Modifiers No. Amount of Amount of IPEC+PESC,Sample a*, MPa starch, state g ~p=3.0 I 0.9 0 dry 0.2 wet 0.1 2 0.9 0.15 dry 0.3 (0.5) wet 0.2 3 0.9 0.3 dry 0.35 (0.6) wet 0.2 4 0.9 0.5 dry 0.4 (0.7) wet 0.2 5 0.9 0.9 dry 0.4 wet 0.2 Cross-linked Interpolyelectrolyte Complexes (#IPEC) In the following examples, the effect of slightly cross-linked polyelectrolyte and linear polyelectrolyte on the mechanical characteristics of the compositions is illustrated. We used the commercial microgel of slightly cross~linked highly water swollen technical poly(acrylic acid) "Carbopol" 2001. The procedure of preparation of gel sample was the following: The predetermined amount of the dry "Carbopol"
was swollen in 300 ml of tap water for five minutes. Then the calculated amount of O.1N aqueous NaOH was added to neutralize the -COOH groups of "CarbopoI" up to the degree of neutralization a=0.33 (the amount ofNaOH added was equal to 33%
relative to the -COON groups of "Carbopol." The partially neutralized "Carbopol"
was additionally swollen in water for 12 hours. The equilibrium degree of swelling, defined as the ratio of the mass of swollen gel to that of the dry gel equaled 1000. The size of the equilibrium swollen microgel particles was about 1 mm.
The standard procedure of preparation of the composition was used: Newsprint (6.6g), mineral wool (4.5g), perlite (17.1 g), and starch (0-18g) were mixed in 500 ml of warm (40°C) 0.002N KCl aqueous solution under stirring. Then 300 ml of partially neutralized "Carbopol" microgel, prepared in advance, was added to the mixture under stirring. Then the predetermined amount of O.1N aqueous solution of PDADMAC was added to make the ratio of total carboxylic groups to ammonium groups equal to 3Ø Since the carboxylic groups were previously one third neutralized, the ratio of neutralized carboxylic groups to ammonium groups thus equals 1Ø Again, an additional amount of water was added to make the total volume equal to 1000 ml. Then 0.018g of flocculant was added last. The mixtures were filtered and prepared in the "brewing regime" as usual. The results of the mechanical testing of the samples are presented in Table 6 and Figure 7.
Table 6 Cross-linked (#) IPEC Data Starch #IPEC Total binderStress at break Stress (g) (g) (g) at break a* dry (Mpa) a* wet (Mpa) Control 0 0.075 0.075 0.25 0.15 _ l 0 0.3 0.3 0.25 0.15 #IPEC
alone 0 0.5 0. 5 0.25 0.15 0 0.9 0.9 0.12 0.07 Control2 0.5 4 _ 0.5 0.15 0.1 Starch 0.9 0 0.9 0.2 0.05 alone (same 1.2 0 1.2 (1.25 0.07 data as in Table 1.8 0 1.8 0.35 0.1 3) 2.7 0 2.7 0.55 0.25 Combination0.5 0.15 0.65 0.25 0.2 0.5 g 0.5 0.3 0.8 _ Starch 0.35 0.2 plus varied0.5 0.5 1 _ 0.35 0.2 #IPEC 0,5 0.9 1.4 0.4 0.2 Combination0.9 0.075 0.975 0.5 0.2 0.9 g 0.9 _ 0.15 1.05 __ 0._55 0.3 Starch 0.9 0.3 1.2 0.4 ~ 0.3 plus varied #IPEC
Combination1.2 0.075 1.275 0.6 0.35 1.2 g 1.2 0.15 1.35 0.5 0.4 Starch 1.2 0.3 1.5 0.4 0.3 plus varied #IPEC
Combination1.8 0.075 1.875 0.8 0.5 ~
1.8 g 1.8 0.15 1.95 0.7 Starch 0.4 plus varied1.8 0.3 2.1 0.45 0.3 #IPEC
While Applicants have set forth embodiments as illustrated and described above, it is recognized that variations may be made with respect to disclosed embodiments. Therefore, while the invention has been disclosed in various forms only, it will be obvious to those skilled in the art that many additions, deletions and modifications can be made without departing from the spirit and scope of this invention, and no undue limits should be imposed except as set forth in the following claims.
The strengthening effect of mixed IPEC+PESC co-binder in "starch brewing"
regime was also tested. Nonstoichiometric mixed IPEC (PAA-PDADMAC) + PESC
(PAA-DDTMAB), cp=3.0 was used. It was prepared as follows:
The predetermined amount of 0.1 N aqueous solution of partially neutralized (a+0,33) poly(acrylic acid) and then correspond-ing amount of 0.04 N aqueous solution of the equimolar mixture of PDADMAC and DDTMAB were added under stirring for about 2-3 minutes.
The compositions containing 0.9 g of the starch binder and different additives of mixed (IPEC+PESC), c~=3.0 co-binder were tested mechanically in the dry and wet S state. The results of the latest measurements are listed in Table 3. Table 3 illustrates the joint action of starch binder and mixed IPEC (PAA-PDADMAC) + PESC (PAA-DDTMAB), cp=3.0 (cp=[PAA]/[DDTMAB+PDADMAC] at [DDTMAB]=[PDADMAC]) co-binder on the mechanical characteristics of the compositions prepared in the "brewing" regime. All samples contained 6.6 g of newsprint, 4.5 g of mineral wool. 17.1 g of perlite and 0.018 g of flocculant.
The samples were tested in dry and wet state.
Table 5 IPEC and PESC Combinations as Starch Modifiers No. Amount of Amount of IPEC+PESC,Sample a*, MPa starch, state g ~p=3.0 I 0.9 0 dry 0.2 wet 0.1 2 0.9 0.15 dry 0.3 (0.5) wet 0.2 3 0.9 0.3 dry 0.35 (0.6) wet 0.2 4 0.9 0.5 dry 0.4 (0.7) wet 0.2 5 0.9 0.9 dry 0.4 wet 0.2 Cross-linked Interpolyelectrolyte Complexes (#IPEC) In the following examples, the effect of slightly cross-linked polyelectrolyte and linear polyelectrolyte on the mechanical characteristics of the compositions is illustrated. We used the commercial microgel of slightly cross~linked highly water swollen technical poly(acrylic acid) "Carbopol" 2001. The procedure of preparation of gel sample was the following: The predetermined amount of the dry "Carbopol"
was swollen in 300 ml of tap water for five minutes. Then the calculated amount of O.1N aqueous NaOH was added to neutralize the -COOH groups of "CarbopoI" up to the degree of neutralization a=0.33 (the amount ofNaOH added was equal to 33%
relative to the -COON groups of "Carbopol." The partially neutralized "Carbopol"
was additionally swollen in water for 12 hours. The equilibrium degree of swelling, defined as the ratio of the mass of swollen gel to that of the dry gel equaled 1000. The size of the equilibrium swollen microgel particles was about 1 mm.
The standard procedure of preparation of the composition was used: Newsprint (6.6g), mineral wool (4.5g), perlite (17.1 g), and starch (0-18g) were mixed in 500 ml of warm (40°C) 0.002N KCl aqueous solution under stirring. Then 300 ml of partially neutralized "Carbopol" microgel, prepared in advance, was added to the mixture under stirring. Then the predetermined amount of O.1N aqueous solution of PDADMAC was added to make the ratio of total carboxylic groups to ammonium groups equal to 3Ø Since the carboxylic groups were previously one third neutralized, the ratio of neutralized carboxylic groups to ammonium groups thus equals 1Ø Again, an additional amount of water was added to make the total volume equal to 1000 ml. Then 0.018g of flocculant was added last. The mixtures were filtered and prepared in the "brewing regime" as usual. The results of the mechanical testing of the samples are presented in Table 6 and Figure 7.
Table 6 Cross-linked (#) IPEC Data Starch #IPEC Total binderStress at break Stress (g) (g) (g) at break a* dry (Mpa) a* wet (Mpa) Control 0 0.075 0.075 0.25 0.15 _ l 0 0.3 0.3 0.25 0.15 #IPEC
alone 0 0.5 0. 5 0.25 0.15 0 0.9 0.9 0.12 0.07 Control2 0.5 4 _ 0.5 0.15 0.1 Starch 0.9 0 0.9 0.2 0.05 alone (same 1.2 0 1.2 (1.25 0.07 data as in Table 1.8 0 1.8 0.35 0.1 3) 2.7 0 2.7 0.55 0.25 Combination0.5 0.15 0.65 0.25 0.2 0.5 g 0.5 0.3 0.8 _ Starch 0.35 0.2 plus varied0.5 0.5 1 _ 0.35 0.2 #IPEC 0,5 0.9 1.4 0.4 0.2 Combination0.9 0.075 0.975 0.5 0.2 0.9 g 0.9 _ 0.15 1.05 __ 0._55 0.3 Starch 0.9 0.3 1.2 0.4 ~ 0.3 plus varied #IPEC
Combination1.2 0.075 1.275 0.6 0.35 1.2 g 1.2 0.15 1.35 0.5 0.4 Starch 1.2 0.3 1.5 0.4 0.3 plus varied #IPEC
Combination1.8 0.075 1.875 0.8 0.5 ~
1.8 g 1.8 0.15 1.95 0.7 Starch 0.4 plus varied1.8 0.3 2.1 0.45 0.3 #IPEC
While Applicants have set forth embodiments as illustrated and described above, it is recognized that variations may be made with respect to disclosed embodiments. Therefore, while the invention has been disclosed in various forms only, it will be obvious to those skilled in the art that many additions, deletions and modifications can be made without departing from the spirit and scope of this invention, and no undue limits should be imposed except as set forth in the following claims.
Claims (43)
1. A polymer binder for a fibrous sheet comprising:
an anionic polymer having a negative charge of between about 4 to about 12 milliequivalents per gram; and a cationic polymer having a positive charge of between about 6 to about 12 milliequivalents per gram.
an anionic polymer having a negative charge of between about 4 to about 12 milliequivalents per gram; and a cationic polymer having a positive charge of between about 6 to about 12 milliequivalents per gram.
2. The binder of claim 1, wherein the molar ratio of total polyanion acid groups to total polycation groups is between about 10:1 to about 1.1:1.
3. The binder of claim 2, wherein the molar ratio of anionic polymer to cationic polymer is about 3:1.
4. The binder of claim 1, wherein the molecular size of the anionic polymer is between about 10,000 to about 900,000 grams per mole.
5. The binder of claim 1, wherein the anionic polymer is crosslinked.
6. The binder of claim 5, wherein the anionic polymer has a crosslinked density of up to about 1 per 50 units.
7. The binder of claim 1, wherein the molecular size of the cationic polymer is between about 10,000 to about 900,000 grams per mole.
8. The binder of claim 1, wherein the binder forms an interpolyelectrolyte complex.
9. The binder of claim 1, further including a spacer selected from the group consisting of a polysaccharide, a hydrogel, a latex and combinations thereof.
10. The binder of claim 9, wherein the polysaccharide comprises starch.
11. The binder of claim 1, further including a surfactant.
12. The binder of claim 11, wherein the surfactant is selected from the group consisting of alkylamines, fatty amines and combinations thereof.
13. The binder of claim 1, wherein anionic polymer to cationic polymer charge ratio is about 1:1.
14. The binder of claim 1, wherein the anionic polymer is selected from the group consisting of polycarbohydrates, polyphosphates, polysulfonates, polysulfates and combinations thereof.
15. The binder of claim 1, wherein the cationic polymer is selected from the group consisting of polymeric amine.
16. The binder of claim 15, wherein the polymeric amine is selected from the group consisting of primary amines, secondary amines, tertiary amines, quaternary amines and combinations thereof.
17. The binder of claim 1, wherein the anionic polymer is weakly acidic.
18. A method of forming a fibrous sheet comprising:
forming a fibrous slurry;
mixing into the fibrous slurry an anionic polymer having a negative charge of between about 4 to about 12 milliequivalents per gram;
mixing into the fibrous slurry a cationic polymer having a positive charge of between about 6 to about 12 milliequivalents per gram; and drying the fibrous sheet to form the fibrous sheet.
forming a fibrous slurry;
mixing into the fibrous slurry an anionic polymer having a negative charge of between about 4 to about 12 milliequivalents per gram;
mixing into the fibrous slurry a cationic polymer having a positive charge of between about 6 to about 12 milliequivalents per gram; and drying the fibrous sheet to form the fibrous sheet.
19. The method of claim 18, wherein the molar ratio of total polyanion acid groups to total polycation groups is between about 10:1 to about 1.1:1.
20. The method of claim 19, wherein the molar ratio of anionic polymer to cationic polymer is about 3:1.
21. The method of claim 18, wherein the molecular size of the anionic polymer is between about 10,000 to about 900,000 grams per mole.
22. The method of claim 18, wherein the molecular size of the cationic polymer is between about 10,000 to about 900,000 grams per mole.
23. The method of claim 18, wherein the binder forms an interpolyelectrolyte complex.
24. The method of claim 18, further including a polysaccharide.
25. The method of claim 24, wherein the polysaccharide comprises starch.
26. The method of claim 18, wherein anionic polymer to cationic polymer charge ratio is about 1:1.
27. The method of claim 18, wherein the anionic polymer is selected from the group consisting of polycarbohydrates, polyphosphates, polysulfonates, polysulfates and combinations thereof.
28. The method of claim 18, wherein the cationic polymer is selected from the group consisting of polymeric amine.
29 29. The method of claim 28, wherein the polymeric amine is selected from the group consisting of primary amines, secondary amines, tertiary amines, quaternary amines and combinations thereof.
30. The method of claim 18, wherein the anionic polymer is weakly acidic.
31. A fibrous sheet comprising:
at least one type of fiber;
an anionic polymer having a negative charge of between about 4 to about 12 milliequivalents per gram; and a cationic polymer having a positive charge of between about 6 to about 12 milliequivalents per gram.
at least one type of fiber;
an anionic polymer having a negative charge of between about 4 to about 12 milliequivalents per gram; and a cationic polymer having a positive charge of between about 6 to about 12 milliequivalents per gram.
32. The fibrous sheet of claim 31, wherein the molar ratio of total polyanion acid groups to total polycation groups is between about 10:1 to about 1.1:1.
33. The fibrous sheet of claim 32, wherein the molar ratio of anionic polymer to cationic polymer is about 3:1.
34. The fibrous sheet of claim 31, wherein the molecular size of the anionic polymer is between about 10,000 to about 900,000 grams per mole.
35. The fibrous sheet of claim 31, wherein the molecular size of the cationic polymer is between about 10,000 to about 900,000 grams per mole.
36. The fibrous sheet of claim 31, wherein the binder forms an interpolyelectrolyte complex.
37. The fibrous sheet of claim 31, further including a polysaccharide.
38. The fibrous sheet of claim 37, wherein the polysaccharide comprises starch.
39. The fibrous sheet of claim 31, wherein anionic polymer to cationic polymer charge ratio is about 1:1.
40. The fibrous sheet of claim 31, wherein the anionic polymer is selected from the group consisting of polycarbohydrates, polyphosphates, polysulfonates, polysulfates and combinations thereof.
41. The fibrous sheet of claim 31, wherein the cationic polymer is selected from the group consisting of polymeric amine.
42. The fibrous sheet of claim 41, wherein the polymeric amine is selected from the group consisting of primary amines, secondary amines, tertiary amines, quaternary amines and combinations thereof.
43. The fibrous sheet of claim 31, wherein the anionic polymer is weakly acidic.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US09/933,408 | 2001-08-20 | ||
US09/933,408 US6755938B2 (en) | 2001-08-20 | 2001-08-20 | Fibrous sheet binders |
Publications (1)
Publication Number | Publication Date |
---|---|
CA2395893A1 true CA2395893A1 (en) | 2003-02-20 |
Family
ID=25463898
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA002395893A Abandoned CA2395893A1 (en) | 2001-08-20 | 2002-07-26 | Fibrous sheet binders |
Country Status (7)
Country | Link |
---|---|
US (3) | US6755938B2 (en) |
EP (1) | EP1285993A1 (en) |
JP (1) | JP2003147691A (en) |
KR (1) | KR20030017363A (en) |
CA (1) | CA2395893A1 (en) |
MX (1) | MXPA02008036A (en) |
RU (1) | RU2318088C2 (en) |
Families Citing this family (40)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1172983C (en) * | 2002-10-28 | 2004-10-27 | 汕头市奇佳机械厂有限公司 | Completely degradable paper-like material with starch as basic material and its prepn |
DE10319738A1 (en) * | 2003-04-30 | 2004-11-18 | Basf Ag | Process for the preparation of aqueous dispersions of polyelectrolyte complexes and their use for increasing the wet strength of paper, cardboard and cardboard |
US20050022956A1 (en) * | 2003-07-29 | 2005-02-03 | Georgia-Pacific Resins Corporation | Anionic-cationic polymer blend for surface size |
US7291275B1 (en) | 2004-04-19 | 2007-11-06 | Davis Robert A | Method for clarifying industrial wastewater while minimizing sludge |
US7799169B2 (en) | 2004-09-01 | 2010-09-21 | Georgia-Pacific Consumer Products Lp | Multi-ply paper product with moisture strike through resistance and method of making the same |
US20060183816A1 (en) * | 2005-02-11 | 2006-08-17 | Gelman Robert A | Additive system for use in paper making and process of using the same |
US20060258248A1 (en) * | 2005-05-11 | 2006-11-16 | Shooshtari Kiarash A | Fiberglass binder comprising epoxidized oil and multifunctional carboxylic acids or anhydrides |
US7960452B2 (en) * | 2005-07-01 | 2011-06-14 | Akzo Nobel Coatings International B.V. | Adhesive composition and method |
US8147979B2 (en) * | 2005-07-01 | 2012-04-03 | Akzo Nobel Coatings International B.V. | Adhesive system and method |
SI2574640T1 (en) * | 2005-07-26 | 2023-05-31 | Knauf Insulation Gmbh | Binders and materials made therewith |
US20070108041A1 (en) * | 2005-11-11 | 2007-05-17 | Guo George X | Magnetron source having increased usage life |
US20090317651A1 (en) * | 2006-06-23 | 2009-12-24 | Akzo Nobel Coatings International B.V. | Adhesive system and method of producing a wood based product |
US8048257B2 (en) * | 2006-06-23 | 2011-11-01 | Akzo Nobel Coating International B.V. | Adhesive system and method of producing a wood based product |
US20080176053A1 (en) * | 2007-01-24 | 2008-07-24 | United States Cypsum Company | Gypsum Wallboard Containing Acoustical Tile |
DK2108006T3 (en) | 2007-01-25 | 2020-12-21 | Knauf Insulation Gmbh | BINDERS AND MATERIALS MADE THEREFORE |
CN101720341B (en) | 2007-01-25 | 2013-06-12 | 克瑙夫绝缘私人有限公司 | Composite wood board |
US20100086726A1 (en) | 2007-01-25 | 2010-04-08 | Roger Jackson | Mineral fibre board |
CA2683706A1 (en) | 2007-04-13 | 2008-10-23 | Knauf Insulation Gmbh | Composite maillard-resole binders |
GB0715100D0 (en) | 2007-08-03 | 2007-09-12 | Knauf Insulation Ltd | Binders |
FR2928383B1 (en) | 2008-03-06 | 2010-12-31 | Georgia Pacific France | WAFER SHEET COMPRISING A PLY IN WATER SOLUBLE MATERIAL AND METHOD FOR PRODUCING SUCH SHEET |
CA2770396A1 (en) | 2009-08-07 | 2011-02-10 | Knauf Insulation | Molasses binder |
JP2013509963A (en) | 2009-11-09 | 2013-03-21 | スポットライト テクノロジー パートナーズ エルエルシー | Fragmented hydrogel |
WO2011057131A1 (en) | 2009-11-09 | 2011-05-12 | Spotlight Technology Partners Llc | Polysaccharide based hydrogels |
CN103025777B (en) | 2010-05-07 | 2016-01-20 | 克瑙夫绝缘私人有限公司 | Carbohydrate binder and the material prepared with it |
EA025773B1 (en) | 2010-05-07 | 2017-01-30 | Кнауф Инзулацьон | Method of making fibers bound by cured polymeric binder, composition and composite wood board |
CA2801546C (en) | 2010-06-07 | 2018-07-10 | Knauf Insulation | Fiber products having temperature control additives |
CA2834816C (en) | 2011-05-07 | 2020-05-12 | Knauf Insulation | Liquid high solids binder composition |
GB201206193D0 (en) | 2012-04-05 | 2012-05-23 | Knauf Insulation Ltd | Binders and associated products |
JP2014034753A (en) * | 2012-08-10 | 2014-02-24 | Rengo Co Ltd | Papermaking additive and method of producing the same |
GB201214734D0 (en) | 2012-08-17 | 2012-10-03 | Knauf Insulation Ltd | Wood board and process for its production |
CA2892900C (en) | 2012-12-05 | 2020-08-11 | Benedicte Pacorel | Method for manufacturing an article comprising a collection of matter bound by a cured binder |
US9347181B2 (en) * | 2013-11-22 | 2016-05-24 | Kemira Oyj | Method for increasing paper strength |
CA2938154C (en) | 2014-02-07 | 2022-11-01 | Knauf Insulation, Inc. | Uncured articles with improved shelf-life |
GB201408909D0 (en) | 2014-05-20 | 2014-07-02 | Knauf Insulation Ltd | Binders |
GB201517867D0 (en) | 2015-10-09 | 2015-11-25 | Knauf Insulation Ltd | Wood particle boards |
GB201610063D0 (en) | 2016-06-09 | 2016-07-27 | Knauf Insulation Ltd | Binders |
GB201701569D0 (en) | 2017-01-31 | 2017-03-15 | Knauf Insulation Ltd | Improved binder compositions and uses thereof |
GB201804907D0 (en) | 2018-03-27 | 2018-05-09 | Knauf Insulation Ltd | Composite products |
GB201804908D0 (en) | 2018-03-27 | 2018-05-09 | Knauf Insulation Ltd | Binder compositions and uses thereof |
CN114768543B (en) * | 2022-03-14 | 2023-04-14 | 德蓝水技术股份有限公司 | Preparation method of anti-pollution reverse osmosis membrane |
Family Cites Families (37)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3049469A (en) | 1957-11-07 | 1962-08-14 | Hercules Powder Co Ltd | Application of coating or impregnating materials to fibrous material |
US2884057A (en) | 1954-02-25 | 1959-04-28 | American Cyanamid Co | Paper of improved dry strength and method of making same |
US2890978A (en) | 1957-10-02 | 1959-06-16 | American Cyanamid Co | Paper of high dry strength and low wet strength |
US2963396A (en) | 1957-12-06 | 1960-12-06 | American Cyanamid Co | High dry strength-low wet strength paper |
US3303184A (en) | 1965-05-25 | 1967-02-07 | Gen Mills Inc | Aminoethyl gums and process for preparing same |
US3332834A (en) | 1965-11-03 | 1967-07-25 | American Cyanamid Co | Process of forming dry strength paper with cationic resin, polyacrylamide resin and alum complex and paper thereof |
US3677888A (en) | 1966-04-29 | 1972-07-18 | American Cyanamid Co | Manufacture of paper using amphoteric strengthening agents |
US3660338A (en) | 1966-04-29 | 1972-05-02 | American Cyanamid Co | Amphoteric strengthening agents for paper |
US3875097A (en) | 1971-12-23 | 1975-04-01 | John Andrew Sedlak | Ionic vinylamide polymer latex and manufacture of paper therewith |
US3874994A (en) | 1971-12-23 | 1975-04-01 | American Cyanamid Co | Process of making paper where an ionic vinylamide polymer latex is added to the furnish to improve dry strength of the paper |
US3840489A (en) | 1971-12-23 | 1974-10-08 | American Cyanamid Co | Novel vinylamide dry strength resins and paper containing the same hydrophilic-hydrophobic vinylamide polymers and manufacture of paper |
US3819555A (en) | 1971-12-23 | 1974-06-25 | American Cyanamid Co | Vinylamide-acrolein polymers and paper of improved strength having a content thereof |
US3875098A (en) | 1971-12-23 | 1975-04-01 | American Cyanamid Co | Ionic vinylamide polymer latex and manufacture of paper therewith |
US4002588A (en) | 1974-05-08 | 1977-01-11 | American Cyanamid Company | Hydrophilic-hydrophobic amphoteric polysalt sizing compositions and paper sized therewith |
US4088530A (en) | 1974-11-05 | 1978-05-09 | Borden Products Limited | Dry strength paper and process therefor |
US4167439A (en) | 1976-12-14 | 1979-09-11 | Rohm And Haas Company | Non-ionic, water-soluble polymers for improving the dry-strength of paper |
CH632546A5 (en) | 1977-08-26 | 1982-10-15 | Ciba Geigy Ag | METHOD FOR PRODUCING SIZED PAPER OR CARDBOARD USING POLYELECTROLYTE AND SALTS OF EPOXYD-AMINE-POLYAMINOAMIDE IMPLEMENTATION PRODUCTS. |
SE443818B (en) | 1978-04-24 | 1986-03-10 | Mitsubishi Chem Ind | PROCEDURE FOR MAKING PAPER WITH IMPROVED DRY STRENGTH |
US4347100A (en) | 1981-05-21 | 1982-08-31 | The Chemithon Corporation | Strength of paper from mechanical or thermomechanical pulp |
US4549931A (en) | 1983-01-27 | 1985-10-29 | Corning Glass Works | Inorganic binders for articles formed from fibers |
US4623428A (en) | 1983-10-27 | 1986-11-18 | Ciba-Geigy Corporation | Process for sizing paper with anionic hydrophobic sizing agents and cationic retention aids |
SE8306739L (en) | 1983-12-06 | 1985-06-07 | Svenska Traeforskningsinst | SET TO MAKE PAPERS WITH HIGH FILLER CONTENT |
DE3583559D1 (en) | 1984-08-15 | 1991-08-29 | Allied Colloids Ltd | WATER-SOLUBLE POLYMERS. |
GB8602121D0 (en) | 1986-01-29 | 1986-03-05 | Allied Colloids Ltd | Paper & paper board |
US4911788A (en) | 1988-06-23 | 1990-03-27 | The Celotex Corporation | Method of wet-forming mineral fiberboard with formation of fiber nodules |
KR0159921B1 (en) | 1988-10-03 | 1999-01-15 | 마이클 비. 키한 | A composition comprising cathionic and anionic polymer process thereof |
US5338406A (en) | 1988-10-03 | 1994-08-16 | Hercules Incorporated | Dry strength additive for paper |
US5134179A (en) | 1988-11-25 | 1992-07-28 | Armstrong World Industries, Inc. | Composite fiberboard and process of manufacture |
US5338407A (en) | 1991-12-23 | 1994-08-16 | Hercules Incorporated | Enhancement of paper dry strength by anionic and cationic guar combination |
US5318669A (en) * | 1991-12-23 | 1994-06-07 | Hercules Incorporated | Enhancement of paper dry strength by anionic and cationic polymer combination |
DE4244194A1 (en) | 1992-12-24 | 1994-06-30 | Basf Ag | Water-soluble condensation products from compounds containing amino groups and crosslinking agents, processes for their preparation and their use |
US6228217B1 (en) * | 1995-01-13 | 2001-05-08 | Hercules Incorporated | Strength of paper made from pulp containing surface active, carboxyl compounds |
DE19701523A1 (en) | 1997-01-17 | 1998-07-23 | Basf Ag | Polymer modified anionic starch, process for its preparation and its use |
JPH10266095A (en) * | 1997-03-25 | 1998-10-06 | Seiko Kagaku Kogyo Co Ltd | Paper surface treatment agent |
US6294645B1 (en) | 1997-07-25 | 2001-09-25 | Hercules Incorporated | Dry-strength system |
JP3383192B2 (en) * | 1997-09-08 | 2003-03-04 | 日本製紙株式会社 | Manufacturing method of molding molding |
SE0001268L (en) | 2000-04-06 | 2001-10-07 | Sca Hygiene Prod Ab | Process for adsorbing successive thin layers of cationic and anionic polymers onto the surface of particles or groups of particles, and paper or nonwoven product containing such particles or groups of particles |
-
2001
- 2001-08-20 US US09/933,408 patent/US6755938B2/en not_active Ceased
-
2002
- 2002-07-26 CA CA002395893A patent/CA2395893A1/en not_active Abandoned
- 2002-08-01 EP EP02017318A patent/EP1285993A1/en not_active Withdrawn
- 2002-08-19 JP JP2002238616A patent/JP2003147691A/en active Pending
- 2002-08-19 MX MXPA02008036A patent/MXPA02008036A/en unknown
- 2002-08-19 RU RU2002122488/04A patent/RU2318088C2/en not_active IP Right Cessation
- 2002-08-20 KR KR1020020049291A patent/KR20030017363A/en not_active Application Discontinuation
- 2002-11-14 US US10/294,179 patent/US6716312B2/en not_active Expired - Fee Related
-
2006
- 2006-06-29 US US11/478,542 patent/USRE42110E1/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
US20030116294A1 (en) | 2003-06-26 |
USRE42110E1 (en) | 2011-02-08 |
KR20030017363A (en) | 2003-03-03 |
US6716312B2 (en) | 2004-04-06 |
US20030075292A1 (en) | 2003-04-24 |
JP2003147691A (en) | 2003-05-21 |
EP1285993A1 (en) | 2003-02-26 |
MXPA02008036A (en) | 2004-12-13 |
US6755938B2 (en) | 2004-06-29 |
RU2318088C2 (en) | 2008-02-27 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CA2395893A1 (en) | Fibrous sheet binders | |
US9752284B2 (en) | Method for treating a fibre stock for making of paper, board or the like and product | |
KR102116873B1 (en) | Papermaking agent system, method for making a papermaking agent system and its use | |
CN103806331B (en) | A kind of composite flame-proof filler and add the fire retardant papers of this fire-retardant filler | |
KR20130096633A (en) | Stable and aqueous compositions of polyvinylamines with cationic starch, and utility for papermaking | |
CA2517275A1 (en) | Starch compositions and methods of making starch compositions | |
KR900006615A (en) | Dry Strength Improvement Additive for Paper | |
US20020117280A1 (en) | Fibrous sheet enhancement | |
EP1448699B1 (en) | Modified starch and process therefor | |
CN104452455A (en) | Papermaking additive composition and method for increasing finished paper ash retention | |
CN108409905A (en) | Acrylamide copolymer of dialdehyde and preparation method thereof | |
CA2550261C (en) | Filler for papermaking process | |
CN102704337A (en) | High-charge-density polymer/AKD(alkyl ketene dimer) instant-curing neutral sizing agent preparation process | |
AU2002346464A1 (en) | Modified starch and process therefor | |
CA2571083A1 (en) | Filler for paper making process | |
KR20060028783A (en) | Gelled starch compositions and methods of making gelled starch compositions | |
KR101435885B1 (en) | Manufacture of environment-friendly mulching paper with inorganic material | |
EP1162208A1 (en) | Derivatized malto-oligosaccharides, methods for trash scavenging, and processes for preparing a paper web | |
JP2502236B2 (en) | Non-combustible sheet | |
JP2006526080A (en) | Modified starch composition | |
CN116905288A (en) | Fluorine-free degradable pulp molding composite material and preparation method thereof | |
RU2095383C1 (en) | Hydrogen-containing bitumen | |
JPS6319475B2 (en) | ||
MXPA01001666A (en) | A process to improve the drainage rate and retention of fines during papermaking |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
FZDE | Dead |